CN102344654A - Hydrolysis resistant PET composite material and preparation method thereof - Google Patents
Hydrolysis resistant PET composite material and preparation method thereof Download PDFInfo
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- CN102344654A CN102344654A CN 201110164262 CN201110164262A CN102344654A CN 102344654 A CN102344654 A CN 102344654A CN 201110164262 CN201110164262 CN 201110164262 CN 201110164262 A CN201110164262 A CN 201110164262A CN 102344654 A CN102344654 A CN 102344654A
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- 238000006460 hydrolysis reaction Methods 0.000 title claims abstract description 78
- 230000007062 hydrolysis Effects 0.000 title claims abstract description 77
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 239000002131 composite material Substances 0.000 title abstract description 8
- 229920005989 resin Polymers 0.000 claims abstract description 46
- 239000011347 resin Substances 0.000 claims abstract description 46
- 238000002156 mixing Methods 0.000 claims abstract description 35
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 31
- 239000002994 raw material Substances 0.000 claims abstract description 28
- 239000004970 Chain extender Substances 0.000 claims abstract description 26
- 239000002667 nucleating agent Substances 0.000 claims abstract description 6
- 239000011521 glass Substances 0.000 claims description 67
- 239000012752 auxiliary agent Substances 0.000 claims description 47
- 239000011159 matrix material Substances 0.000 claims description 37
- -1 dihydroxyphenyl Chemical group 0.000 claims description 27
- 239000003381 stabilizer Substances 0.000 claims description 27
- 239000000314 lubricant Substances 0.000 claims description 14
- 238000005469 granulation Methods 0.000 claims description 13
- 230000003179 granulation Effects 0.000 claims description 13
- HVLLSGMXQDNUAL-UHFFFAOYSA-N triphenyl phosphite Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)OC1=CC=CC=C1 HVLLSGMXQDNUAL-UHFFFAOYSA-N 0.000 claims description 8
- ANSXAPJVJOKRDJ-UHFFFAOYSA-N furo[3,4-f][2]benzofuran-1,3,5,7-tetrone Chemical group C1=C2C(=O)OC(=O)C2=CC2=C1C(=O)OC2=O ANSXAPJVJOKRDJ-UHFFFAOYSA-N 0.000 claims description 7
- PEPBFCOIJRULGJ-UHFFFAOYSA-N 3h-1,2,3-benzodioxazole Chemical compound C1=CC=C2NOOC2=C1 PEPBFCOIJRULGJ-UHFFFAOYSA-N 0.000 claims description 5
- 239000004593 Epoxy Substances 0.000 claims description 4
- 150000001336 alkenes Chemical class 0.000 claims description 2
- 229920000578 graft copolymer Polymers 0.000 claims description 2
- 239000000178 monomer Substances 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- ZJOLCKGSXLIVAA-UHFFFAOYSA-N ethene;octadecanamide Chemical group C=C.CCCCCCCCCCCCCCCCCC(N)=O.CCCCCCCCCCCCCCCCCC(N)=O ZJOLCKGSXLIVAA-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 4
- 239000003365 glass fiber Substances 0.000 abstract description 3
- 239000012760 heat stabilizer Substances 0.000 abstract 2
- 239000004615 ingredient Substances 0.000 abstract 2
- 230000004927 fusion Effects 0.000 abstract 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 84
- 239000005020 polyethylene terephthalate Substances 0.000 description 84
- 238000001125 extrusion Methods 0.000 description 18
- RKISUIUJZGSLEV-UHFFFAOYSA-N n-[2-(octadecanoylamino)ethyl]octadecanamide Chemical group CCCCCCCCCCCCCCCCCC(=O)NCCNC(=O)CCCCCCCCCCCCCCCCC RKISUIUJZGSLEV-UHFFFAOYSA-N 0.000 description 10
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 9
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229920006351 engineering plastic Polymers 0.000 description 2
- 125000004185 ester group Chemical group 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006225 ethylene-methyl acrylate Polymers 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- FTQWRYSLUYAIRQ-UHFFFAOYSA-N n-[(octadecanoylamino)methyl]octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NCNC(=O)CCCCCCCCCCCCCCCCC FTQWRYSLUYAIRQ-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
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Abstract
The invention provides a hydrolysis resistant PET composite material, comprising ingredients by weight of: 40-65% of PET resin, 30-50% of glass fiber, 0.1-1% of hydrolysis resistant agent, 0.3-1.5% of chain extender, 0.3-1% of heat stabilizer, 1-2% of nucleating agent and 3-5% of accessory ingredient. The invention also provides a preparation method of the hydrolysis resistant PET composite material. The method comprises steps of: selecting raw materials according to the weight percentage; mixing well the PET resin, the hydrolysis resistant agent, the chain extender, the heat stabilizer, the nucleating agent and the accessory agent to obtain a mixed raw material; putting the mixed raw material in a double screw extruder, mixing, extruding by fusion, granulating to obtain the hydrolysis resistant PET composite material. The hydrolysis resistant PET composite material has good hydrolysis resistance and high stability.
Description
Technical field
The invention belongs to technical field of polymer materials, be specifically related to a kind of hydrolysis PET matrix material and preparation method thereof.
Background technology
Polyethylene terephthalate (PET) has cheap, has characteristics such as good wear resistance, thermotolerance, chemical proofing, electrical insulating property and mechanical strength height, therefore, has just begun the application and development as engineering plastics the sixties in 20th century.The PET engineering plastics have been applied to industries such as automobile, motor, electronics, household electrical appliance and machinery at present.
Because the PET resin contains ester group; And ester group is very responsive to hydrolysis under higher temperature, when having moisture to exist; Become very obvious at hydrolysis reaction more than 160 ℃ especially, cause PET Material Physics mechanical property to descend rapidly, this drawbacks limit the application of PET under hygrothermal environment.
Summary of the invention
The embodiment of the invention provides a kind of hydrolysis PET matrix material and preparation method thereof, is intended to solve the problem of PET resin hydrolyzing in the prior art.
A kind of hydrolysis PET matrix material, it comprises the following component according to weight percent:
PET resin 40～65%;
Spun glass 30～50%;
Hydrolysis agent 0.1～1%;
Chainextender 0.3～1.5%;
Thermo-stabilizer 0.3～1%;
Nucleator 1～2%;
Auxiliary agent 3～5%.
And, a kind of preparation method of hydrolysis PET matrix material, it comprises the steps:
Choose raw material according to weight percent, said raw material comprises PET resin 40～65%, spun glass 30～50%, hydrolysis agent 0.1～1%, chainextender 0.3～1.5%, thermo-stabilizer 0.3～1%, nucleator 1～2%, auxiliary agent 3～5%;
PET resin, hydrolysis agent, chainextender, thermo-stabilizer, nucleator and auxiliary agent are mixed, get mixing raw material;
Above-mentioned mixing raw material is placed twin screw extruder and spun glass blending, and through melt extruding, granulation obtains said hydrolysis PET matrix material.
The hydrolysis PET matrix material that the embodiment of the invention provides through adopting the rationally composite of spun glass, hydrolysis agent and thermo-stabilizer, improves heat-resisting, the hydrolysis ability of PET material.Further, the preparation method of this hydrolysis PET matrix material adopts the technology of the disposable completion of mixing reaction extruding pelletization, and its preparation method technology is simple, and is easy to operate, high efficiency, and cost is low, is suitable for suitability for industrialized production.
Description of drawings
Fig. 1 is preparing method's schema of preparation method of the hydrolysis PET matrix material of the embodiment of the invention.
Embodiment
In order to make the object of the invention, technical scheme and advantage clearer,, the present invention is further elaborated below in conjunction with accompanying drawing and embodiment.Should be appreciated that specific embodiment described herein only in order to explanation the present invention, and be not used in qualification the present invention.
A kind of hydrolysis PET matrix material of the embodiment of the invention, it comprises the following component according to weight percent:
PET resin 40～65%;
Spun glass 30～50%;
Hydrolysis agent 0.1～1%;
Chainextender 0.3～1.5%;
Thermo-stabilizer 0.3～1%;
Nucleator 1～2%;
Auxiliary agent 3～5%.
The specific density of said PET resin (polyethylene terephthalate) is 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is 0.6～0.8PS.
Said spun glass is preferably the E-CR spun glass, and filament diameter is 5～13 μ m.The E-CR spun glass is a kind of improved no boron non-alkali glass, and its water tolerance is improved 7～8 times than alkali-free glass fiber, and acid resistance is more superior than medium-alkali glass fiber.As, commercially available
952A.
Said hydrolysis agent is preferably polycarbodiimide, as, commercially available Stabaxol KE 7646.The polycarbodiimide tool space aromatic structure that is obstructed generates unsettled midbody with the end carboxyl reaction, then resets to be stable and neutral N-acylurea, thereby has improved the anti-hydrolytic performance of PET resin.
Said chainextender is preferably pyromellitic acid dianhydride, gathers benzo-dioxazole, in bis-epoxy dihydroxyphenyl propane-diglycidylether and the triphenyl phosphite any one.
Said thermo-stabilizer be preferably phosphorous acid dihydroxyphenyl propane ester or four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate.
Said nucleator is preferably the heterogeneous nucleation agent, and this is because the heterogeneous nucleation agent can not reduce the molecular weight of PET resin.For example, 2000-3000 order talcum powder, heterogeneous nucleation agent such as nano kaoline and nano imvite.
Said auxiliary agent comprises toughner and lubricant.Toughner is preferably the graft copolymer of ethylene-like polymer alkene and acrylic ester monomer, like ethylene-methyl methacrylate butyl ester-glycidyl acrylate multipolymer, ethylene-methyl acrylate copolymer, Vilaterm octene-glycidyl acrylate multipolymer etc.Lubricant is preferably ethylene bis stearamide and verivate thereof.Ethylene bis stearic amide molecule two ends are nonpolar chain alkyl, and the centre is a polarity bisamide base, and this symmetrical meta polar structure is given its good wetting and penetrating power.All kinds of weighting agents there is significant wetting and dissemination.In the PET resin, have good consistency, and demonstrate good inside and outside lubricant effect.
See also Fig. 1, show the preparation method of the hydrolysis PET matrix material of the embodiment of the invention, this method comprises the steps:
S01: choose raw material according to weight percent, said raw material comprises PET resin 40～65%, spun glass 30～50%, hydrolysis agent 0.1～1%, chainextender 0.3～1.5%, thermo-stabilizer 0.3～1%, nucleator 1～2%, auxiliary agent 3～5%;
S02: PET resin, hydrolysis agent, chainextender, thermo-stabilizer, nucleator and auxiliary agent are mixed, get mixing raw material;
S03: above-mentioned mixing raw material is placed twin screw extruder and spun glass blending, and through melt extruding, granulation obtains said hydrolysis PET matrix material.
Among the step S01, all material weighings are accurate, are accurate to 0.001 kilogram, put into corresponding material bag and carry out sign.
Step S02 is specially, and PET resin, hydrolysis agent, chainextender, thermo-stabilizer, nucleator and auxiliary agent were added in the moderate-speed mixers premix 3～7 minutes, mixing raw material.
Among the step S03, with above-mentioned mixing raw material and spun glass blending, through melt extruding granulation.This mixture and the spun glass temperature of each section in twin screw extruder is preferably respectively: 220～260 ℃ of district's temperature; Two district's temperature are 220～260 ℃; 220～260 ℃ of three district's temperature; 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 1～3 minute.
The hydrolysis PET matrix material that the embodiment of the invention provides is selected the E-CR spun glass for use, and its water resistance is good, through agent of choose reasonable hydrolysis and thermo-stabilizer, obtains the stronger PET matrix material of heat-resisting hydrolysis ability simultaneously.Additive therefor is commercially available, and production cost is low, and said hydrolysis PET process for producing composite material is simple, easily control.The hydrolysis PET matrix material that obtains can partly substitute the nylon products that uses under the hygrothermal environment.
Below embodiment through concrete prescription and preparation method above-mentioned hydrolysis PET matrix material and preparation method thereof is described.
Embodiment 1:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 63.1%;
Spun glass 30%;
Hydrolysis agent 0.3%;
Chainextender 0.3%;
Thermo-stabilizer 0.3%;
Nucleator 2%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is a pyromellitic acid dianhydride; Said thermo-stabilizer is a phosphorous acid dihydroxyphenyl propane ester; Said nucleator is 2500 purpose talcum powder, and said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 63.1%, polycarbodiimide 0.3%, pyromellitic acid dianhydride 0.3%; Phosphorous acid dihydroxyphenyl propane ester 0.3%; 2500 order talcum powder 2% and other auxiliary agents 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 30% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Embodiment 2:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 62.4%;
Spun glass 30%;
Hydrolysis agent 0.5%;
Chainextender 0.6%;
Thermo-stabilizer 0.5%;
Nucleator 2%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is for gathering benzo-dioxazole; Said thermo-stabilizer is a phosphorous acid dihydroxyphenyl propane ester; Said nucleator is 2500 purpose talcum powder, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 62.4%, polycarbodiimide 0.5% gathers benzo-dioxazole 0.6%; Phosphorous acid dihydroxyphenyl propane ester 0.5%; 2500 order talcum powder 2% and other auxiliary agents 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 30% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Embodiment 3:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 61.7%;
Spun glass 30%;
Hydrolysis agent 0.8%;
Chainextender 1%;
Thermo-stabilizer 1%;
Nucleator 1.5%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is bis-epoxy dihydroxyphenyl propane-diglycidylether; Said thermo-stabilizer be four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate; Said nucleator is a nano kaoline, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 61.7%, polycarbodiimide 0.8%, bis-epoxy dihydroxyphenyl propane-diglycidylether 1%; Four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate 1%; Nano kaoline 1.5% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 30% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Embodiment 4:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 61%;
Spun glass 30%;
Hydrolysis agent 1%;
Chainextender 1.5%;
Thermo-stabilizer 1%;
Nucleator 1.5%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is a triphenyl phosphite; Said thermo-stabilizer be four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate; Said nucleator is a nano kaoline, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 61%, polycarbodiimide 1%, triphenyl phosphite 1.5%; Four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate 1%; Nano kaoline 1.5% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 30% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Embodiment 5:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 53.3%;
Spun glass 40%;
Hydrolysis agent 0.6%;
Chainextender 0.6%;
Thermo-stabilizer 0.5%;
Nucleator 1%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is a pyromellitic acid dianhydride; Said thermo-stabilizer is a phosphorous acid dihydroxyphenyl propane ester; Said nucleator is a nano kaoline, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 53.3%, polycarbodiimide 0.6%, pyromellitic acid dianhydride 0.6%; Phosphorous acid dihydroxyphenyl propane ester 0.5%; Nano kaoline 1% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 40% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Embodiment 6:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 43.6%;
Spun glass 50%;
Hydrolysis agent 0.6%;
Chainextender 0.3%;
Thermo-stabilizer 0.5%;
Nucleator 1%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is the E-CR spun glass; Said hydrolysis agent is a polycarbodiimide; Said chainextender is a pyromellitic acid dianhydride; Said thermo-stabilizer is a phosphorous acid dihydroxyphenyl propane ester; Said nucleator is a nano imvite, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 43.6%, polycarbodiimide 0.6% gathers benzo-dioxazole 0.3%; Phosphorous acid dihydroxyphenyl propane ester 0.5%; Nano imvite 1% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press; Add 50% E-CR spun glass, granulation in the extrusion at screw rod middle part.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Comparative Examples 1:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 64%;
Spun glass 30%;
Nucleator 2%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is preferably the E spun glass; Said nucleator is 2500 order talcum powder, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 64%, 2500 order talcum powder 2% and other auxiliary agent 4%, middling speed stirrer for mixing 5 minutes, extrude through screw extrusion press, add 30% E spun glass in the extrusion at the screw rod middle part, granulation.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Comparative Examples 2:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 55%;
Spun glass 40%;
Nucleator 1%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is preferably the E spun glass; Said nucleator is a nano kaoline, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 55%, nano kaoline 1% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press, add 40% E spun glass in the extrusion at the screw rod middle part, granulation.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Comparative Examples 3:
The component and the weight percentage thereof of the hydrolysis PET matrix material of present embodiment are:
PET resin 45%;
Spun glass 50%;
Nucleator 1%;
Auxiliary agent 4%.
Wherein, said PET resin is a specific density 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is the polyethylene terephthalate of 0.6～0.8PS; Said spun glass is preferably the E spun glass; Said nucleator is a nano imvite, and said auxiliary agent is that said auxiliary agent is toughner POE graft glycidyl methacrylate and lubricant ethylene bis stearamide.
With weight percent PET resin 45%, nano imvite 1% and other auxiliary agent 4% middling speed stirrer for mixing 5 minutes, are extruded through screw extrusion press, add 50% E spun glass in the extrusion at the screw rod middle part, granulation.Wherein, 220～260 ℃ of district's temperature, two district's temperature are 220～260 ℃, 220～260 ℃ of three district's temperature, 220～260 ℃ of four district's temperature, mixing raw material and spun glass time of delivery in screw rod is 2 minutes.
Will be by the hydrolysis PET matrix material of embodiment 1～6 and Comparative Examples 1～3 preparation under 120～130 ℃ of conditions dry 3～5 hours, and then the particulate material that drying is good carries out the injection molding sample preparation on injector, carry out performance test.
The batten of preparation carries out the hydrolysis test with PCT high pressure deterioration accelerator, and the PCT test condition is: 120 ℃ of temperature, humidity 100%R.H. takes out the conservation rate of its physical and mechanical properties of cooling back test after 168 hours.The performance of embodiment 1～6 and Comparative Examples 1～3 is respectively shown in table 1 and table 2.
Table 1
Table 2
The data that contrast in above-mentioned table 1 and the table 2 can draw, and the present invention is through the hydrolysis spun glass, and hydrolysis-resisting agent and thermo-stabilizer rationally composite is significantly increased the hydrolysis ability of PET.
The above is merely preferred embodiment of the present invention, not in order to restriction the present invention, all any modifications of within spirit of the present invention and principle, being done, is equal to and replaces and improvement etc., all should be included within protection scope of the present invention.
Claims (10)
1. a hydrolysis PET matrix material is characterized in that, comprises the following component according to weight percent:
PET resin 40～65%;
Spun glass 30～50%;
Hydrolysis agent 0.1～1%;
Chainextender 0.3～1.5%;
Thermo-stabilizer 0.3～1%;
Nucleator 1～2%;
Auxiliary agent 3～5%.
2. hydrolysis PET matrix material as claimed in claim 1 is characterized in that the specific density of said PET resin is 1.35～1.38, and fusing point is 255 ℃～260 ℃, and kinetic viscosity is 0.6～0.8PS.
3. hydrolysis PET matrix material as claimed in claim 1 is characterized in that said spun glass is the E-CR spun glass.
4. hydrolysis PET matrix material as claimed in claim 1 is characterized in that said hydrolysis agent is a polycarbodiimide.
5. hydrolysis PET matrix material as claimed in claim 1 is characterized in that, said chainextender is pyromellitic acid dianhydride, gather at least a in benzo-dioxazole, bis-epoxy dihydroxyphenyl propane-diglycidylether, the triphenyl phosphite.
6. hydrolysis PET matrix material as claimed in claim 1 is characterized in that, said thermo-stabilizer be phosphorous acid dihydroxyphenyl propane ester and/or four (2,4-di-tert-butyl-phenyl-4,4 '-xenyl) biphosphonate.
7. hydrolysis PET matrix material as claimed in claim 1 is characterized in that said nucleator is the heterogeneous nucleation agent.
8. hydrolysis PET matrix material as claimed in claim 1; It is characterized in that; Said auxiliary agent comprises toughner and lubricant, and said toughner is the graft copolymer of ethylene-like polymer alkene and acrylic ester monomer, and said lubricant is ethylene bis stearic amide and verivate thereof.
9. the preparation method of a hydrolysis PET matrix material, it comprises the steps:
Choose raw material according to weight percent, said raw material comprises PET resin 40～65%, spun glass 30～50%, hydrolysis agent 0.1～1%, chainextender 0.3～1.5%, thermo-stabilizer 0.3～1%, nucleator 1～2%, auxiliary agent 3～5%;
PET resin, hydrolysis agent, chainextender, thermo-stabilizer, nucleator and auxiliary agent are mixed, get mixing raw material;
Above-mentioned mixing raw material is placed twin screw extruder and spun glass blending, and through melt extruding, granulation obtains said hydrolysis PET matrix material.
10. the preparation method of hydrolysis PET matrix material as claimed in claim 9 is characterized in that, the temperature of said twin screw extruder is 220～260 ℃, and mixing raw material and spun glass time of delivery in screw rod is 1～3 minute.
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| CN104233502A (en) * | 2013-06-20 | 2014-12-24 | 东丽纤维研究所（中国）有限公司 | Hydrolysis-resistant polyester fiber and preparation method thereof |
| CN104695045A (en) * | 2015-04-03 | 2015-06-10 | 太仓市三丰化纤有限公司 | Preparation method for improved medium-high strength PET fibers |
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| CN113429758A (en) * | 2021-07-13 | 2021-09-24 | 江阴市龙山合成材料有限公司 | Hydrolysis-resistant and anti-aging PET modified material and preparation method thereof |
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| CN110172235A (en) * | 2019-06-19 | 2019-08-27 | 广州市聚赛龙工程塑料股份有限公司 | A kind of hydrolysis-resistant low-warpage PBT composite and its preparation method and application |
| CN113429758A (en) * | 2021-07-13 | 2021-09-24 | 江阴市龙山合成材料有限公司 | Hydrolysis-resistant and anti-aging PET modified material and preparation method thereof |
| CN114395223A (en) * | 2021-12-28 | 2022-04-26 | 上海普利特复合材料股份有限公司 | Hydrolysis-resistant, high-weather-resistance and high-strength glass fiber reinforced PP/PET material for photovoltaic back plate and preparation method thereof |
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